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Appendices 10.A & 10.B: An Educational Presentation. Presented By: Joseph Ash Jordan Baldwin Justin Hirt Andrea Lance. History of Heat Conduction. Jean Baptiste Biot (1774-1862) French Physicist Worked on analysis of heat conduction

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appendices 10 a 10 b an educational presentation

Appendices 10.A & 10.B:An Educational Presentation

Presented By:

Joseph Ash

Jordan Baldwin

Justin Hirt

Andrea Lance

history of heat conduction
History of Heat Conduction

Jean Baptiste Biot

  • (1774-1862)
    • French Physicist
    • Worked on analysis of heat conduction
    • Unsuccessful at dealing with the problem of incorporating external convection effects in heat conduction analysis
history of heat conduction3
History of Heat Conduction

Jean Baptiste Joseph Fourier

  • (1768 – 1830)
  • Read Biot’s work
  • 1807 determined how to solve the problem
  • Fourier’s Law
    • Time rate of heat flow (Q) through a slab is proportional to the gradient of

temperature difference

history of heat conduction4
History of Heat Conduction

Ernst Schmidt

  • German scientist
  • Pioneer in Engineering Thermodynamics
  • Published paper “Graphical Difference Method for Unsteady Heat Conduction”
  • First to measure velocity and temperature field in free convection boundary layer and large heat transfer coefficients
  • Schmidt Number
    • Analogy between heat and mass

transfer that causes a dimensionless

quantity

derivation of the heat conduction equation

Derivation of the Heat Conduction Equation

A first approximation of the equations that govern the conduction of heat in a solid rod.

consider the following
Consider the following:
  • A uniform rod is insulated on both lateral ends.
    • Heat can now only flow in the axial direction.
  • It is proven that heat per unit time will pass from the warmer section to the cooler one.
  • The amount of heat is proportional to the area, A, and to the temperature difference T2-T1, and is inversely proportional to the separation distance, d.
slide7
The final consideration can be expressed as the following:

is a proportionality factor called the thermal conductivity and is determined by material properties

assumptions
Assumptions
  • The bar has a length L so x=0 and x=L
  • Perfectly insulated
  • Temperature, u, depends only on position, x, and time, t
    • Usually valid when the lateral dimensions are small compared to the total length.
slide9
The differential equation governing the temperature of the bar is a physical balance between two rates:
    • Flux/Flow term
    • Absorption term
slide10
Flux
  • The instantaneous rate of heat transfer from left to right across the cross sections x=x0where x0 is arbitrary can be defined as:
  • The negative is needed in order to show a positive rate from left to right (hot to cold)
slide11
Flux
  • Similarly, the instantaneous rate of heat transfer from right to left across the cross section x=x0+Δx where Δx is small can be defined as:
slide12
Flux
  • The amount of heat entering the bar in a time span of Δt is found by subtracting the previous two equations and then multiplying the result by Δt:
heat absorption
Heat Absorption
  • The average change in temperature, Δu, can be written in terms of the heat introduced, Q Δt and the mass Δm of the element as:

where s = specific heat of the material

ρ = density

heat absorption14
Heat Absorption
  • The actual temperature change of the bar is simply the actual change in temperature at some intermediate point, so the above equation can also be written as:

This is the heat absorption equation.

heat equation
Heat Equation
  • Equating the QΔt in the flux and absorption terms, we find the heat absorption equation to be:
slide16
If we divide the above equation by ΔxΔt and allow both Δx and Δt to both go to 0, we will obtain the heat conduction or diffusion equation:

where

and has the dimensions of length^2/time and called the thermal diffusivity

boundary conditions
Boundary Conditions
  • Certain boundary conditions may apply to the specific heat conduction problem, for example:
    • If one end is maintained at some constant temperature value, then the boundary condition for that end is u = T.
    • If one end is perfectly insulated, then the boundary condition stipulates ux = 0.
generalized boundary conditions
Generalized Boundary Conditions
  • Consider the end where x=0 and the rate of flow of heat is proportional to the temperature at the end of the bar.
    • Recall that the rate of flow will be given, from left to right, as
    • With this said, the rate of heat flow out of the bar from right to left will be
    • Therefore, the boundary condition at x=0 is

where h1 is a proportionality constant

if h1=0, then it corresponds to an insulated end

if h1 goes to infinity, then the end is held at 0 temp.

generalized boundary conditions19
Generalized Boundary Conditions
  • Similarly, if heat flow occurs at the end x = L, then the boundary condition is as follows:

where, again, h2 is a nonzero proportionality factor

initial boundary condition
Initial Boundary Condition
  • Finally, the temperature distribution at one fixed instant – usually taken at t = 0, takes the form:

occurring throughout the bar

generalizations
Generalizations
  • Sometimes, the thermal conductivity, density, specific heat, or area may change as the axial position changes. The rate of heat transfer under such conditions at x=x0 is now:
  • The heat equation then becomes a partial differential equation in the form:

or

generalizations22
Generalizations
  • Other ways for heat to enter or leave a bar must also be taken into consideration.
  • Assume G(x,t,u) is a rate per unit per time.
    • Source
      • G(x,t,u) is added to the bar
      • G(x,t,u) is positive, non-zero, linear, and u does not depend on t
      • G(x,t,u) must be added to the left side of the heat equation yielding the following differential equation
generalizations23
Generalizations
  • Similarly,
    • Sink
      • G(x,t,u) is subtracted from the bar
      • G(x,t,u) is positive, non-zero, linear, and u does not depend on t
      • G(x,t,u) then under this sink condition takes the form:
generalizations24
Generalizations
  • Putting the source and sink equations together in the heat equation yields

which is commonly called the generalized heat conduction equation

multi dimensional space
Multi-dimensional space
  • Now consider a bar in which the temperature is a function of more than just the axial x-direction. Then the heat conduction equation can then be written:
    • 2-D:
    • 3-D:
example 1 section 10 6 problem 9
Example 1: Section 10.6, Problem 9

Let an aluminum rod of length 20 cm be initially at the uniform temperature 25C. Suppose that at time t=0, the end x=0 is cooled to 0C while the end x=20 is heated to 60C, and both are thereafter maintained at those temperatures.

Find the temperature distribution in the rod at any time t

example 1 section 10 6 problem 927
Example 1: Section 10.6, Problem 9

Find the temperature distribution, u(x,t)

2uxx=ut, 0<x<20, t<0

u(0,t)=0 u(20,t)=60, t<0

u(x,0)=25, 0<x<20

From the initial equation we find that:

L=20, T1=0, T2=60, f(x)=25

We look up the Thermal Diffusivity of aluminum→2=0.86

example 1 section 10 6 problem 928
Example 1: Section 10.6, Problem 9

Using Equations 16 and 17 found on page 614, we find that

where

example 1 section 10 6 problem 929
Example 1: Section 10.6, Problem 9

Evaluating cn, we find that

example 1 section 10 6 problem 930
Example 1: Section 10.6, Problem 9

Now we can solve for u(x,t)

slide32

Derivation of the Wave Equation

  • Applicable for:
    • One space dimension, transverse vibrations on elastic string
    • Endpoints at x = 0 and x = L along the x-axis
    • Set in motion at t = 0 and then left undisturbed
equation derivation
Equation Derivation

Since there is no acceleration in the horizontal direction

However the vertical components must satisfy

where is the coordinate to the center of mass and the weight is neglected

Replacing T with V the and rearranging the equation becomes

derivation continued
Derivation continued

Letting , the equation becomes

To express this in terms of only terms of u we note that

The resulting equation in terms of u is

and since H(t) is not dependant on x the resulting equation is

derivation continued36
Derivation Continued

For small motions of the string, it is approximated that

using the substitution that

the wave equation takes its customary form of

wave equation generalizations
Wave Equation Generalizations

The telegraph equation

where c and k are nonnegative constants

cut arises from a viscous damping force

ku arises from an elastic restoring force

F(x,t) arises from an external force

The differences between this telegraph equation and the customary

wave equation are due to the consideration of internal elastic

forces. This equation also governs flow of voltage or current in a

transmission line, where the coefficients are related to the electrical

parameters in the line.

wave equations in additional dimensions
Wave Equations in Additional Dimensions

For a vibrating system with more than on significant space coordinate it may be necessary to consider the wave equation in more than one dimension.

For two dimensions the wave equation becomes

For three dimensions the wave equation becomes

example 2 section 10 7 problem 6
Example 2: Section 10.7, Problem 6

Consider an elastic string of length L whose ends are held fixed. The string is set in motion from its equilibrium position with an initial velocity g(x). Let L=10 and a=1. Find the string displacement for any time t.

example 2 section 10 7 problem 640
Example 2: Section 10.7, Problem 6

From equations 35 and 36 on page 631, we find that

where

example 2 section 10 7 problem 641
Example 2: Section 10.7, Problem 6

Solving for kn, we find:

example 2 section 10 7 problem 642
Example 2: Section 10.7, Problem 6

Now we can solve for u(x,t)